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公开(公告)号:US20250091862A1
公开(公告)日:2025-03-20
申请号:US18965188
申请日:2024-12-02
Applicant: Haldor Topsøe A/S
Inventor: Sudip DE SARKAR , Thomas Sandahl CHRISTENSEN , Martin ØSTBERG , Kim AASBERG-PETERSEN
Abstract: A plant, such as a hydrocarbon plant, is provided, which has a syngas stage for syngas generation and a synthesis stage where the syngas is synthesized to produce syngas derived product, such as hydrocarbon product. The plant makes effective use of various streams; in particular, CO2 and H2. The plant does not comprise an external feed of hydrocarbons. A method for producing a product stream, such as a hydrocarbon product stream is also provided.
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公开(公告)号:US12246964B2
公开(公告)日:2025-03-11
申请号:US17641293
申请日:2020-09-24
Applicant: HALDOR TOPSØE A/S
Inventor: Peter Mølgaard Mortensen , Kasper Emil Larsen , Kim Aasberg-Petersen , Robert Klein
Abstract: A reactor system and a process for carrying out the methanol cracking reaction of a feedstock comprising methanol to hydrogen are provided, where the heat for the endothermic methanol cracking reaction is provided by resistance heating.
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公开(公告)号:US12246299B2
公开(公告)日:2025-03-11
申请号:US17776142
申请日:2020-11-11
Applicant: HALDOR TOPSØE A/S
Inventor: Peter Mølgaard Mortensen
Abstract: A reactor system and a process for carrying out steam cracking of a feed gas comprising hydrocarbons is provided, i where the heat for the reaction is provided by resistance heating by means of electrical power, so that a product stream comprising at least one olefin compound is obtained.
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公开(公告)号:US12227473B2
公开(公告)日:2025-02-18
申请号:US17821967
申请日:2022-08-24
Applicant: HALDOR TOPSØE A/S
Inventor: Christian Mårup Osmundsen , Morten Boberg Larsen
Abstract: A process for the production of glycolaldehyde by thermolytic fragmentation of a carbohydrate feedstock including mono- and/or di-saccharide(s) and a system suitable for performing the process. The process and the system are suitable for industrial application, and the process may be performed in a continuous process. The salt-depleted carbohydrate feedstock may include one or more impurities selected from the group of arsenic, lead, sulfate, sulfur dioxide, and 5-(hydroxymethyl)furfural.
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公开(公告)号:US20240350996A1
公开(公告)日:2024-10-24
申请号:US18761285
申请日:2024-07-01
Applicant: HALDOR TOPSØE A/S
Inventor: Peter Mølgaard MORTENSEN , Kim AASBERG-PETERSEN
CPC classification number: B01J8/067 , B01J8/025 , B01J8/0465 , B01J19/12 , B01J19/244 , C01B3/384 , B01J2208/00433 , C01B2203/0233 , C01B2203/0283 , C01B2203/0855 , C01B2203/1241
Abstract: A chemical reactor including reformer tubes for reforming a first feed stream including a hydrocarbon gas and steam. The chemical reactor includes one or more reformer tubes arranged to being heated by an electrically driven heat source. The reformer tube includes a first inlet for feeding said first feed stream into a first reforming reaction zone of the reformer tube, and a feed conduit arranged to allow a second feed stream into a second reforming reaction zone of the reformer tube. The second reforming reaction zone is positioned downstream of the first reforming reaction zone. The feed conduit is configured so that the second feed stream is only in contact with catalyst material in the second reforming reaction zone. A process of producing CO rich synthesis gas at low S/C conditions.
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公开(公告)号:US11760718B2
公开(公告)日:2023-09-19
申请号:US16469841
申请日:2018-02-01
Applicant: HALDOR TOPSØE A/S
IPC: C07C253/16 , B01J21/04 , B01J23/835 , C01C3/02
CPC classification number: C07C253/16 , B01J21/04 , B01J23/835 , C01C3/0241
Abstract: The invention relates to a process for producing a product gas comprising acetonitrile and/or hydrogen cyanide from a feed stream comprising ammonia and methanol over a solid catalyst comprising a support, a first metal and a second metal on the support, wherein the first metal and the second metal are in the form of a chemical compound, wherein the first metal is Fe, Ru or Co and the second metal is Sn, Zn, or Ge. The pressure is ambient pressure or higher and the temperature lies in a range from about 400° C. to about 700° C. Thus, the process for producing acetonitrile and/or hydrogen cyanide from ammonia and methanol may be catalyzed by a single catalyst and may be carried out in a single reactor. The invention also relates to a catalyst, a method for activating a catalyst and use of a catalyst for catalysing production of acetonitrile and/or hydrogen cyanide from ammonia and methanol.
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公开(公告)号:US20230226516A1
公开(公告)日:2023-07-20
申请号:US18001274
申请日:2021-07-15
Applicant: HALDOR TOPSØE A/S
Inventor: Peter Mølgaard MORTENSEN , Sebastian Thor WISMANN , Kasper Emil LARSEN , Anders Helbo HANSEN
IPC: B01J19/24
CPC classification number: B01J19/2485 , B01J19/249 , B01J2219/2416 , B01J2219/2428 , B01J2219/2434 , B01J2219/2438
Abstract: A structured catalyst for catalyzing an endothermic reaction of a feed gas to convert it to a product gas is provided.
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公开(公告)号:US11691877B2
公开(公告)日:2023-07-04
申请号:US17594680
申请日:2020-04-30
Applicant: HALDOR TOPSØE A/S
Inventor: Morten Thellefsen , Per Aggerholm Sørensen , Martin Møllerhøj , Mads Lykke
IPC: C01B17/02 , C01B17/04 , C01B17/80 , B01D53/86 , B01J19/00 , B01J19/24 , C01B17/775 , B01D53/14 , C01B17/76 , F23G7/06
CPC classification number: C01B17/0404 , B01D53/1481 , B01D53/1493 , B01D53/8615 , B01J19/0013 , B01J19/2405 , B01J19/2465 , C01B17/0253 , C01B17/0447 , C01B17/0452 , C01B17/0456 , C01B17/76 , C01B17/775 , C01B17/80 , C01B17/806 , F23G7/06 , B01D2255/20723 , B01J2219/00157 , C01P2006/80 , F23G2209/14
Abstract: A process plant and a process for production of sulfur from a feedstock gas including from 15% to 100 vol % H2S and a stream of sulfuric acid, the process including a) providing a Claus reaction furnace feed stream with a substoichiometric amount of oxygen, b) directing to a Claus reaction furnace operating at elevated temperature, c) cooling to provide a cooled Claus converter feed gas, d) directing to contact a material catalytically active in the Claus reaction, e) withdrawing a Claus tail gas and elementary sulfur, f) directing a stream comprising said Claus tail gas to a Claus tail gas treatment, wherein sulfuric acid directed to said Claus reaction furnace is in the form of droplets with 90% of the mass of the droplets having a diameter below 500 μm, with the associated benefit of such a process efficiently converting all liquid H2SO4 to gaseous H2SO4 and further to SO2.
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公开(公告)号:US11618677B2
公开(公告)日:2023-04-04
申请号:US17606557
申请日:2020-04-29
Applicant: HALDOR TOPSØE A/S
Inventor: Morten Thellefsen , Mads Lykke , Martin Møllerhøj
IPC: B01D53/86 , C01B17/04 , C01B17/80 , C01B17/02 , B01J19/00 , B01J19/24 , C01B17/775 , B01D53/14 , C01B17/76 , F23G7/06
Abstract: A revamp process for modifying a sulfur abatement plant including a Claus process plant, the Claus process plant including a Claus reaction furnace and one or more Claus conversion stages, each Claus conversion stage including a conversion reactor and a means for elemental sulfur condensation, and a means of Claus tail gas oxidation configured for receiving a Claus tail gas from said Claus process plant and configured for providing an oxidized Claus tail gas, the process revamp including: a) providing a sulfuric acid producing tail gas treatment plant producing sulfuric acid, and b) providing a means for transferring an amount or all of the sulfuric acid produced in said sulfuric acid producing tail gas treatment plant to said Claus reaction furnace, wherein the moles of sulfur in the transferred sulfuric acid relative to the moles of elemental sulfur withdrawn from the Claus process plant is from 3% to 25%.
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公开(公告)号:US11591215B2
公开(公告)日:2023-02-28
申请号:US17049040
申请日:2019-05-15
Applicant: HALDOR TOPSØE A/S
Inventor: Peter Mølgaard Mortensen , Kim Aasberg-Petersen , Robert Klein
IPC: C01B3/38 , B01D53/26 , B01J19/00 , B01J19/24 , B01J35/00 , B01J35/04 , C01B3/40 , C01B3/50 , B01D53/047 , B01D53/14 , B01D53/22
Abstract: A hydrogen plant for producing hydrogen, including: a reforming reactor system including a first catalyst bed including an electrically conductive material and a catalytically active material, a heat insulation layer between the first catalyst bed and the pressure shell, and at least two conductors electrically connected to the electrically conductive material and to an electrical power supply placed outside the pressure shell, wherein the electrical power supply is dimensioned to heat at least part of the first catalyst bed to a temperature of at least 500° C. by passing an electrical current through the electrically conductive material, where the pressure shell has a design pressure of between 5 and 200 bar; a water gas shift unit downstream the reforming reactor system; and a gas separation unit downstream the water gas shift unit. A process for producing hydrogen from a feed gas including hydrocarbons.
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